US8299282B2 - Continuous method for the heterogenically catalyzed esterification of fatty acids - Google Patents
Continuous method for the heterogenically catalyzed esterification of fatty acids Download PDFInfo
- Publication number
- US8299282B2 US8299282B2 US12/738,115 US73811508A US8299282B2 US 8299282 B2 US8299282 B2 US 8299282B2 US 73811508 A US73811508 A US 73811508A US 8299282 B2 US8299282 B2 US 8299282B2
- Authority
- US
- United States
- Prior art keywords
- process according
- fatty acids
- free fatty
- catalyst
- alcohol
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related, expires
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
- C07C67/03—Preparation of carboxylic acid esters by reacting an ester group with a hydroxy group
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
- C07C67/08—Preparation of carboxylic acid esters by reacting carboxylic acids or symmetrical anhydrides with the hydroxy or O-metal group of organic compounds
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11C—FATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
- C11C3/00—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
- C11C3/003—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fatty acids with alcohols
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11C—FATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
- C11C3/00—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
- C11C3/04—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fats or fatty oils
- C11C3/10—Ester interchange
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
Definitions
- DE 196 00 025 discloses, inter alia, that it may be advantageous to add additional free fatty acids to the pre-esterification. Under some circumstances, this can serve to reduce the relative proportion by mass of inert material in the starting material of the process.
- no fundamental solution to the technical problem of achieving higher conversions and consequent increased space-time yields of a pre-esterification is disclosed, since, more particularly, the free fatty acids used for the increase in the proportion of the free fatty acids preferably stem from a later process step and are therefore subjected to further processing steps. This is especially true because soap cleavage by means of metered addition of homogeneously dissolved acids becomes necessary here.
- the maximum space-time yield disclosed in DE 196 00 025 is 34 g of fatty acid methyl ester per litre of reactor volume and hour.
- starting materials are all fats and/or oils which include at least a proportion of free fatty acids, and a proportion of fatty acid glycerides. Preference is given to starting materials which possess a proportion of free fatty acids greater than 2% by weight.
- alcohols refer to mono- or polyhydric C 1 to C 5 alcohols or mixtures thereof Preference is given to monohydric C 1 to C 3 alcohols. Very particular preference is given to methanol.
- the hydricity of an alcohol describes the number of covalently bonded hydroxyl groups present in the inventive alcohol.
- the conversion of free fatty acids at the outlet of the second reaction stage is at least 90% based on the stream from the first reaction stage ( 5 ) and at least 99.5% based on the stream into the first reaction stage ( 3 ).
- the stream ( 9 ) of the free fatty acids which have thus been converted to alkyl esters is added, in a mixer ( 60 ), in step 6) of the process according to the invention, to the stream ( 11 ) of starting material which stems from the reaction stage ( 20 ) for transesterification and has likewise been converted to alkyl esters, so as to obtain, for example, a stream of biodiesel ( 12 ).
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Fats And Perfumes (AREA)
- Catalysts (AREA)
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE102007052065 | 2007-10-30 | ||
| DE102007052065A DE102007052065A1 (de) | 2007-10-30 | 2007-10-30 | Kontinuierliches Verfahren zur heterogen katalysierten Veresterung von Fettsäuren |
| DE102007052065.6 | 2007-10-30 | ||
| PCT/EP2008/008763 WO2009056231A1 (de) | 2007-10-30 | 2008-10-16 | Kontinuierliches verfahren zur heterogen katalysierten veresterung von fettsäuren |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| US20100249442A1 US20100249442A1 (en) | 2010-09-30 |
| US8299282B2 true US8299282B2 (en) | 2012-10-30 |
Family
ID=40292442
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US12/738,115 Expired - Fee Related US8299282B2 (en) | 2007-10-30 | 2008-10-16 | Continuous method for the heterogenically catalyzed esterification of fatty acids |
Country Status (22)
| Country | Link |
|---|---|
| US (1) | US8299282B2 (OSRAM) |
| EP (1) | EP2205708A1 (OSRAM) |
| CN (1) | CN101842471B (OSRAM) |
| AR (1) | AR071058A1 (OSRAM) |
| AU (1) | AU2008318001A1 (OSRAM) |
| BR (1) | BRPI0819144A8 (OSRAM) |
| CA (1) | CA2703813A1 (OSRAM) |
| CO (1) | CO6270372A2 (OSRAM) |
| CR (1) | CR11400A (OSRAM) |
| DE (1) | DE102007052065A1 (OSRAM) |
| EA (1) | EA018797B1 (OSRAM) |
| HN (1) | HN2010000893A (OSRAM) |
| IL (1) | IL204938A (OSRAM) |
| MX (1) | MX2010004519A (OSRAM) |
| NI (1) | NI201000073A (OSRAM) |
| NZ (1) | NZ584970A (OSRAM) |
| PA (1) | PA8799301A1 (OSRAM) |
| PE (1) | PE20090934A1 (OSRAM) |
| SV (1) | SV2010003551A (OSRAM) |
| UY (1) | UY31390A1 (OSRAM) |
| WO (1) | WO2009056231A1 (OSRAM) |
| ZA (1) | ZA201002942B (OSRAM) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8957242B2 (en) | 2013-03-15 | 2015-02-17 | Renewable Energy Group, Inc. | Dual catalyst esterification |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP2522712A1 (en) * | 2011-05-13 | 2012-11-14 | Cognis IP Management GmbH | Process for obtaining fatty acid lower alkyl esters from unrefined fats and oils |
| US9738842B2 (en) * | 2013-06-19 | 2017-08-22 | Argent Energy (Uk) Limited | Process and apparatus for purifying a fatty mixture and related products including fuels |
| FR3015515B1 (fr) | 2013-12-19 | 2016-02-05 | IFP Energies Nouvelles | Procede de pretraitement d'huiles vegetales par catalyse heterogene de l'esterification des acides gras |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB384715A (en) * | 1931-08-31 | 1932-12-15 | Ig Farbenindustrie Ag | Apparatus for carrying out the manufacture and production of neutral products from oiats |
| DE1960002A1 (de) | 1968-12-04 | 1970-06-18 | Jean Joseph Alfred Beyl | Sicherheitsskibindung |
| GB2145079A (en) * | 1983-08-17 | 1985-03-20 | Nisshin Oil Mills Ltd | Methyl-esterification of deodorisation distillates of oils |
| EP0192035A2 (de) | 1985-01-21 | 1986-08-27 | Henkel Kommanditgesellschaft auf Aktien | Verfahren zur Vorveresterung freier Fettsäuren in Rohfetten und/oder -ölen |
| DE19600025A1 (de) | 1996-01-03 | 1997-07-10 | Henkel Kgaa | Verfahren zur Herstellung von Fettstoffen |
| US20050113589A1 (en) * | 2003-10-14 | 2005-05-26 | Kao Corporation | Process for producing a fatty acid ester |
| WO2007083213A2 (en) | 2006-01-19 | 2007-07-26 | Merloni Progetti S.P.A. | Process for the preparation of biodiesel |
| WO2007093326A1 (en) | 2006-02-15 | 2007-08-23 | Aser S.R.L. | Method for deacidifying oils and/or fats |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1865401A (zh) * | 2006-06-19 | 2006-11-22 | 菏泽华瑞油脂有限责任公司 | 高酸价棉籽油制取生物柴油的方法 |
| CN101016473B (zh) * | 2007-03-02 | 2012-04-18 | 安徽省粮油科学研究所 | 劣质油生产生物燃料油的方法 |
| CN101058734B (zh) * | 2007-05-31 | 2010-12-01 | 张付舜 | 工业化微波合成生物柴油的装置及其方法 |
-
2007
- 2007-10-30 DE DE102007052065A patent/DE102007052065A1/de not_active Withdrawn
-
2008
- 2008-10-14 UY UY31390A patent/UY31390A1/es not_active Application Discontinuation
- 2008-10-16 BR BRPI0819144A patent/BRPI0819144A8/pt not_active IP Right Cessation
- 2008-10-16 EP EP08844944A patent/EP2205708A1/de not_active Withdrawn
- 2008-10-16 PA PA20088799301A patent/PA8799301A1/es unknown
- 2008-10-16 EA EA201000582A patent/EA018797B1/ru not_active IP Right Cessation
- 2008-10-16 MX MX2010004519A patent/MX2010004519A/es active IP Right Grant
- 2008-10-16 AU AU2008318001A patent/AU2008318001A1/en not_active Abandoned
- 2008-10-16 CN CN200880113695.7A patent/CN101842471B/zh not_active Expired - Fee Related
- 2008-10-16 WO PCT/EP2008/008763 patent/WO2009056231A1/de not_active Ceased
- 2008-10-16 US US12/738,115 patent/US8299282B2/en not_active Expired - Fee Related
- 2008-10-16 CA CA2703813A patent/CA2703813A1/en not_active Abandoned
- 2008-10-16 NZ NZ584970A patent/NZ584970A/en not_active IP Right Cessation
- 2008-10-17 PE PE2008001787A patent/PE20090934A1/es not_active Application Discontinuation
- 2008-10-29 AR ARP080104719A patent/AR071058A1/es not_active Application Discontinuation
-
2010
- 2010-04-08 IL IL204938A patent/IL204938A/en not_active IP Right Cessation
- 2010-04-27 NI NI201000073A patent/NI201000073A/es unknown
- 2010-04-28 HN HN2010000893A patent/HN2010000893A/es unknown
- 2010-04-28 CR CR11400A patent/CR11400A/es not_active Application Discontinuation
- 2010-04-28 ZA ZA2010/02942A patent/ZA201002942B/en unknown
- 2010-04-28 SV SV2010003551A patent/SV2010003551A/es not_active Application Discontinuation
- 2010-04-28 CO CO10050348A patent/CO6270372A2/es active IP Right Grant
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB384715A (en) * | 1931-08-31 | 1932-12-15 | Ig Farbenindustrie Ag | Apparatus for carrying out the manufacture and production of neutral products from oiats |
| DE1960002A1 (de) | 1968-12-04 | 1970-06-18 | Jean Joseph Alfred Beyl | Sicherheitsskibindung |
| GB2145079A (en) * | 1983-08-17 | 1985-03-20 | Nisshin Oil Mills Ltd | Methyl-esterification of deodorisation distillates of oils |
| EP0192035A2 (de) | 1985-01-21 | 1986-08-27 | Henkel Kommanditgesellschaft auf Aktien | Verfahren zur Vorveresterung freier Fettsäuren in Rohfetten und/oder -ölen |
| US4698186A (en) | 1985-01-21 | 1987-10-06 | Henkel Kommanditgesellschaft Auf Aktien | Process for the pre-esterification of free fatty acids in fats and oils |
| DE19600025A1 (de) | 1996-01-03 | 1997-07-10 | Henkel Kgaa | Verfahren zur Herstellung von Fettstoffen |
| US20050113589A1 (en) * | 2003-10-14 | 2005-05-26 | Kao Corporation | Process for producing a fatty acid ester |
| WO2007083213A2 (en) | 2006-01-19 | 2007-07-26 | Merloni Progetti S.P.A. | Process for the preparation of biodiesel |
| WO2007093326A1 (en) | 2006-02-15 | 2007-08-23 | Aser S.R.L. | Method for deacidifying oils and/or fats |
Non-Patent Citations (5)
| Title |
|---|
| Athanassiadis, A., et al., The deacidification of Vegetable oils by distillation during deodorization, 1988, Fat. Sci. Technol., vol. 90, No. 13, pp. 522-526. * |
| DIN EN ISO 2114 Plastics (polyester resins) and paints and varnishes (binders)-Determination of partial acid value and total acid value (ISO 2114:2000). |
| Henkel KGGA, Preparation of fatty acids with low acid values, useful as precursors for esterification, 1997, English translation of DE19600025, 11 pages. * |
| Martinello, M., et al., Grape seed oil deacidification by molecular distillation: Analysis of operative variables influence using the response surfact methodology, 2006, Journal of Food Engineering, vol. 81. pp. 60-64. * |
| Mittelbach, Remschmidt, Biodiesel-The comprehensive handbook 3rd ed., 2006, p. 60. |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8957242B2 (en) | 2013-03-15 | 2015-02-17 | Renewable Energy Group, Inc. | Dual catalyst esterification |
Also Published As
| Publication number | Publication date |
|---|---|
| NI201000073A (es) | 2010-09-23 |
| US20100249442A1 (en) | 2010-09-30 |
| PA8799301A1 (es) | 2009-06-23 |
| PE20090934A1 (es) | 2009-07-24 |
| IL204938A (en) | 2013-12-31 |
| HN2010000893A (es) | 2013-06-24 |
| CN101842471B (zh) | 2014-12-10 |
| ZA201002942B (en) | 2011-07-27 |
| EP2205708A1 (de) | 2010-07-14 |
| BRPI0819144A8 (pt) | 2016-04-26 |
| BRPI0819144A2 (OSRAM) | 2009-05-07 |
| AU2008318001A1 (en) | 2009-05-07 |
| DE102007052065A1 (de) | 2009-05-07 |
| EA018797B1 (ru) | 2013-10-30 |
| CN101842471A (zh) | 2010-09-22 |
| CA2703813A1 (en) | 2009-05-07 |
| AR071058A1 (es) | 2010-05-26 |
| UY31390A1 (es) | 2009-05-29 |
| WO2009056231A1 (de) | 2009-05-07 |
| CR11400A (es) | 2010-11-02 |
| NZ584970A (en) | 2012-06-29 |
| CO6270372A2 (es) | 2011-04-20 |
| SV2010003551A (es) | 2011-08-11 |
| MX2010004519A (es) | 2010-05-14 |
| EA201000582A1 (ru) | 2010-10-29 |
| IL204938A0 (en) | 2010-11-30 |
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| Date | Code | Title | Description |
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| AS | Assignment |
Owner name: BAYER TECHNOLOGY SERVICES GMBH, GERMANY Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:HEINZ, DIETER, DR.;MLECZKO, LESLAW, DR.;ROY, SHAIBAL, DR.;AND OTHERS;SIGNING DATES FROM 20100414 TO 20100507;REEL/FRAME:024428/0276 |
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Free format text: PATENTED CASE |
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Owner name: BAYER INTELLECTUAL PROPERTY GMBH, GERMANY Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:BAYER TECHNOLOGY SERVICES GMBH;REEL/FRAME:031157/0347 Effective date: 20130812 |
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Owner name: ROHM AND HAAS CHEMICALS LLC, PENNSYLVANIA Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:BAYER INTELLECTUAL PROPERTY GMBH;REEL/FRAME:032652/0667 Effective date: 20140401 |
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